EP3035418B1 - Matière active composite pour des batteries rechargeables au lithium et procédé de fabrication de cette dernière - Google Patents

Matière active composite pour des batteries rechargeables au lithium et procédé de fabrication de cette dernière Download PDF

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EP3035418B1
EP3035418B1 EP14836628.9A EP14836628A EP3035418B1 EP 3035418 B1 EP3035418 B1 EP 3035418B1 EP 14836628 A EP14836628 A EP 14836628A EP 3035418 B1 EP3035418 B1 EP 3035418B1
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active material
graphite
lithium secondary
composite active
composite
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EP3035418A4 (fr
EP3035418A1 (fr
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Ryo Tamaki
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Tosoh Corp
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Tosoh Corp
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    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/58—Selection of substances as active materials, active masses, active liquids of inorganic compounds other than oxides or hydroxides, e.g. sulfides, selenides, tellurides, halogenides or LiCoFy; of polyanionic structures, e.g. phosphates, silicates or borates
    • H01M4/583—Carbonaceous material, e.g. graphite-intercalation compounds or CFx
    • H01M4/587—Carbonaceous material, e.g. graphite-intercalation compounds or CFx for inserting or intercalating light metals
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00—Secondary cells; Manufacture thereof
    • H01M10/05—Accumulators with non-aqueous electrolyte
    • H01M10/052—Li-accumulators
    • H01M10/0525—Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/04—Processes of manufacture in general
    • H01M4/0471—Processes of manufacture in general involving thermal treatment, e.g. firing, sintering, backing particulate active material, thermal decomposition, pyrolysis
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/13—Electrodes for accumulators with non-aqueous electrolyte, e.g. for lithium-accumulators; Processes of manufacture thereof
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/362—Composites
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/362—Composites
    • H01M4/364—Composites as mixtures
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/362—Composites
    • H01M4/366—Composites as layered products
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/38—Selection of substances as active materials, active masses, active liquids of elements or alloys
    • H01M4/386—Silicon or alloys based on silicon
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/483—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides for non-aqueous cells
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M4/36—Selection of substances as active materials, active masses, active liquids
    • H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
    • H01M4/485—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of mixed oxides or hydroxides for inserting or intercalating light metals, e.g. LiTi2O4 or LiTi2OxFy
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00—Electrodes
    • H01M4/02—Electrodes composed of, or comprising, active material
    • H01M2004/026—Electrodes composed of, or comprising, active material characterised by the polarity
    • H01M2004/027—Negative electrodes
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10—Energy storage using batteries

Definitions

  • the present invention relates to a composite active material for lithium secondary batteries and a production method therefor.
  • lithium ion secondary batteries lithium secondary batteries
  • anode material determines basic battery characteristics
  • anode materials with better characteristics such as charging and discharging characteristics are being actively developed.
  • Patent Document 1 discloses a composite active material for lithium secondary batteries capable of producing a lithium secondary battery having a large charging and discharging capacity, high-speed charging and discharging characteristics, and good cycle characteristics, as well as a production method therefor.
  • Patent Literature 1 Japanese Patent No. 5227483B
  • JP 2012 124115 A discloses a negative electrode active material for nonaqueous electrolyte secondary battery, said material being a composite particle containing first particles, for example spherical graphite particles, and second particles containing silicon atom, wherein said first and second particles are combined/integrated with a carbonaceous substance derived from a carbon precursor as a binder, wherein the content of Si on the outer surface of the composite particle is much higher than in the core part of the composite particle.
  • JP 2007 059213 A discloses a composite active material for an anode of a lithium secondary battery, said composite material comprising a composite containing Si and SiO 2 , with Si dispersed in SiO 2 , and a carbonaceous substance which comprises graphite component, wherein SiO 2 and graphite component are dispersed in the carbonaceous substance, and wherein the main surface of the composite active material is the carbonaceous substance.
  • US 2006/068287 A1 discloses a negative electrode active material for a nonaqueous electrolyte secondary battery comprising composite particles having a structure in which Si and SiO 2 are dispersed in a carbonaceous matrix that may be graphite, said composite particles being coated with a carbon coating layer that is different from graphite.
  • an object of the present invention is to provide a composite active material for lithium secondary batteries capable of producing an electrode material in which volume expansion is suppressed even after repeated charging and discharging, and capable of producing a lithium secondary battery exhibiting excellent cycle characteristics, as well as a production method therefor.
  • Another object of the present invention is to provide a battery that uses this composite active material for lithium secondary batteries.
  • a composite active material for lithium secondary batteries exhibiting the desired characteristics is obtained by using silicon monoxide and a carbon precursor as the raw materials of production of a composite active material for lithium secondary batteries.
  • the present invention can provide a composite active material for lithium secondary batteries capable of producing an electrode material in which volume expansion is suppressed even after repeated charging and discharging, and capable of producing a lithium secondary battery exhibiting excellent cycle characteristics, as well as a production method therefor.
  • the present invention can provide a battery that uses this composite active material for lithium secondary batteries.
  • FIG. 1 is a schematic cross-sectional view of an embodiment of the composite active material for lithium secondary batteries of the present invention.
  • the composite active material for lithium secondary batteries and production method therefor of the present invention will be described in detail below.
  • One feature of the production method of the present invention is that graphite having a prescribed specific surface area as well as silicon monoxide and a carbon precursor are used as starting raw materials of a composite active material for lithium secondary batteries.
  • silicon which is a battery active material capable of combining with lithium ions, gradually oxides and becomes sponge-like.
  • the cause of oxidation of the silicon is surmised to be a process which occurs repeatedly when lithium ions are accumulated in and released from the silicon, wherein stress is applied to the silicon and cracking occurs, and electrolyte permeates in from these cracks when volume expansion and contraction occur.
  • a spherical mixture in which silicon monoxide is encapsulated in a graphite component is obtained by performing a mixing step and conglobation treatment to be described later using silicon monoxide.
  • this mixture is heat-treated, the following reaction proceeds, and a composite containing silicon dioxide (SiO 2 ) and silicon (Si) (silicon-containing composite) is obtained.
  • the obtained composite has the characteristic that stress does not tend to be applied to the silicon because the silicon consists of fine crystals (preferably not greater than 100 nm), and cracking does not tend to occur even with repeated expansion and contraction. Therefore, oxidation by the electrolyte occurs only on the surface, and advancement of oxidation by the electrolyte into the interior is averted. Furthermore, the majority of the fine silicon surface obtained in the mode described above is protected by silicon dioxide, and oxidation by the electrolyte as described above tends not to occur; this is also considered to result in a contribution to suppression of volume expansion of the electrode materials.
  • the carbon precursor used in conjunction functions as an adhesive between the graphite component and the aforementioned composite, and has the function in aiding electrical contact between the two. As a result, the cycle characteristics of the lithium secondary battery are further improved.
  • composite active material for lithium secondary batteries of the present invention also referred to simply as “composite active material” hereinafter
  • modes of the produced composite active material for lithium secondary batteries will be described in detail.
  • the production method for composite active material for lithium secondary batteries of the present invention has a mixing step of mixing prescribed components; a conglobation step of performing conglobation treatment on the obtained mixture; and a heating step of heat-treating the obtained spherical mixture.
  • the mixing step is a step in which graphite having a specific surface area of not less than 30 m 2 /g, silicon monoxide, and a carbon precursor are mixed to obtain a mixture.
  • a mixture in which silicon monoxide is uniformly blended across an extremely large graphite surface and silicon monoxide is dispersed to an extremely high degree can be obtained.
  • the carbon precursor serves the purpose of aiding adhesion between the graphite and the silicon monoxide at that time.
  • the silicon monoxide and carbon precursor dispersed on and attached to the graphite surface in the mixture becomes enveloped (in other words, encapsulated) in the graphite in a form where it is sandwiched by the graphite, simply by slight pressure being applied to the graphite.
  • the graphite used in this step has a specific surface area of not less than 30 m 2 /g. As long as it is within this range, a composite active material for lithium secondary batteries in which silicon is highly dispersed on the graphite surface having high surface area (and preferably thin) is obtained. As a result, the battery material that uses the composite active material for lithium secondary batteries of the present invention exhibits excellent battery characteristics (for example, high-speed charging and discharging characteristics, large charging and discharging capacity, good cycle characteristics, and the like).
  • the specific surface area is preferably not less than 40 m 2 /g and more preferably not less than 60 m 2 /g because the cycle characteristics of a lithium secondary battery that uses the composite active material are better.
  • the upper limit is not particularly limited, but the specific surface area is preferably not greater than 200 m 2 /g because otherwise, the production procedure becomes complex and synthesis is difficult.
  • the specific surface area of graphite is measured using the BET method by nitrogen adsorption (JIS Z 8830, single-point method).
  • the graphite contains layers consisting of multiple graphene sheets stacked in the direction in which the graphite planes are stacked, and the graphene sheets are bonded to each other primarily by van der Waals forces.
  • the average thickness of the layer of laminated graphene sheets contained in the graphite having the above prescribed specific surface area is preferably not greater than 29 nm and more preferably not greater than 22 nm, because the charging and discharging quantity and the cycle characteristics of a lithium secondary battery that uses the composite active material are better.
  • the lower limit is not particularly limited but is normally not less than 4.4 nm in many cases because otherwise, the production procedure becomes complex.
  • the graphite is observed by electron microscope (TEM) and the thickness of the laminated graphene sheet layer in the graphite is measured at not less than 10 locations, and the average thickness is obtained by taking the arithmetic mean of those values.
  • TEM electron microscope
  • the upper limit of bulk specific gravity of the graphite used is not particularly limited but is preferably not greater than 0.02 g/cm 3 and more preferably not greater than 0.01 g/cm 3 because the composite is more uniform and more highly dispersed in the graphite component in the composite active material. Due to problems in production, the lower limit is often not less than 0.005 g/cm 3 .
  • a sample is inserted in a 500-mL glass graduated cylinder so as not to compress it, and bulk specific gravity is determined by dividing the sample weight by the sample volume.
  • graphite used in this step a commercially available product may be used or graphite may be produced by a known method.
  • Expanded graphite may be produced by, for example, soaking graphite (for example, scaly graphite) in an acid at room temperature and then heat-treating (for example, treating at 700 to 1000°C) the obtained acid-treated graphite. More specifically, scaly natural graphite is soaked for approximately 1 hour in a mixed acid of 9 parts by weight of sulfuric acid and 1 part by weight of nitric acid, and then the acid is removed and the resultant graphite is washed and dried. The obtained acid-treated graphite is then put into a furnace at approximately 850°C to obtain expanded graphite. Expanded graphite may also be obtained when graphite that has formed an intercalation compound of graphite and an alkali metal or the like is used.
  • the bulk density of the acid-treated graphite obtained as described above is not particularly limited but is preferably not less than 0.6 g/cm 3 and more preferably not less than 0.7 g/cm 3 because the acid-treated graphite expands sufficiently.
  • the upper limit is not particularly limited but is often not greater than 1.0 g/cm 3 due to problems in production otherwise.
  • a sample is inserted in a 100-mL glass graduated cylinder so as not to compress it, and bulk density is determined by dividing the sample weight by the sample volume.
  • the above expanded graphite is dispersed in a solvent, and by treating it with ultrasonic treatment or a crusher that applies high shear stress (for example, a millstone), the hinge parts of the expanded graphite are destroyed and flake graphite in which approximately 50 graphene sheets (preferably from 10 to 150 sheets) are laminated is obtained.
  • the silicon monoxide used in this step functions as a precursor that produces silicon, which is the battery active material capable of combining with lithium ions. More specifically, a composite (silicon-containing composite) of silicon (Si) and silicon dioxide (SiO 2 ) is obtained by heat-treating a spherical mixture containing silicon monoxide in the heating step to be described later.
  • SiO x (0.8 ⁇ x ⁇ 1.5) is preferably used as the silicon monoxide.
  • the use of SiO (x ⁇ 1) is particularly desirable because the quantitative relationship between silicon and silicon dioxide is the preferred ratio.
  • the shape of the silicon monoxide used is not particularly limited, and any shape such as powder, plates, granules, fibers, lumps, and spheres may be used.
  • the average particle size of the silicon monoxide used is preferably not greater than 1 ⁇ m, more preferably not greater than 0.5 ⁇ m, and even more preferably not greater than 0.3 ⁇ m because sloughing off of silicon monoxide when forming the composite with graphite as well as expansion and destruction of silicon accompanying cycling can be further suppressed and because there are a greater number of electrical contact points with the graphite.
  • the lower limit is not particularly limited and is preferably low, but is normally not less than 0.1 ⁇ m in many cases.
  • Laser diffraction-style particle size distribution measurement equipment is used to measure average particle size. More specifically, D50 (50% volume particle diameter) is used as the average particle size.
  • silicon monoxide particles of the above prescribed small particle size may be obtained by crushing silicon monoxide using a known apparatus such as a mixing tank-type agitation mill (bead mill or the like).
  • the carbon precursor used in this step functions as an adhesive that increases adhesion between the graphite and the silicon monoxide in the mixture.
  • the carbon precursor is converted to a carbide (for example, hard carbon, soft carbon, non-crystalline carbon, or the like).
  • the carbon precursor is not particularly limited as long as it is a material that is converted to a carbide by heat treatment (baking carbonization) as described above.
  • Examples include polymer compounds (organic polymers), coal-based pitch, petroleum-based pitch, mesophase pitch, coke, low-molecular-weight oil, derivatives thereof, and the like.
  • polymer compounds are preferred because expansion of a battery material that uses the composite active material for lithium secondary batteries is further suppressed and the cycle characteristics for lithium secondary batteries of such a material are better (also stated simply as "because the effects of the present invention are better" hereinafter).
  • polymer compound examples include phenol resin, furan resin, epoxy resin, polyvinyl chloride, polyvinyl alcohol, polyacrylamide, polyethyleneimide, cellulose, rayon, polyacrylonitrile, polystyrene, and the like.
  • One type of carbon precursor may be used alone or two or more types may be used in combination.
  • the shape of the carbon precursor used is not particularly limited, and any shape such as powder, plates, granules, fibers, lumps, and spheres may be used. These carbon precursors are preferably dissolved in the solvent used when mixing the silicone monoxide and the expanded graphite.
  • the average molecular weight of the carbon precursor used is preferably not less than 1000 and more preferably not greater than 1,000,000 because the effects of the present invention are better.
  • the method for mixing the above-described graphite, silicon monoxide, and carbon precursor is not particularly limited, and known methods such as so-called dry processes, wet processes, or the like may be used. Wet processes are preferred because the graphite, silicon monoxide, and carbon precursor in the obtained mixture are more uniformly mixed.
  • An example of a dry process is to add the above-described graphite, silicon monoxide, and carbon precursor and mix them in a known stirring device (for example, a Henschel mixer).
  • An example of a wet process is to disperse the above-described graphite, silicon monoxide, and carbon precursor in a solvent, stir and mix the obtained solution, and remove the solvent.
  • the type of solvent used in wet processes is not particularly limited, and should be a solvent that can disperse graphite, silicon monoxide, and carbon precursor.
  • examples include alcohol-based solvents (for example, methanol, ethanol, isopropanol), ketone-based solvents (for example, acetone, methyl ethyl ketone, cyclohexane), amide-based solvents (for example, formamide, dimethylacetamide, N-methylpyrrolidone, N-ethylpyrrolidone), nitrile-based solvents (for example, acetonitrile, propionitrile), ester-based solvents (for example, methyl acetate, ethyl acetate), carbonate-based solvents (for example, dimethyl carbonate, diethyl carbonate), ether-based solvents (for example, cellosolve), halogen-based solvents, water, mixtures thereof, and the like.
  • alcohol-based solvents for example,
  • an alcohol-based solvent is preferred because the cycle characteristics of a lithium secondary battery that uses the obtained composite active material for lithium secondary batteries are better.
  • the conditions of mixing and stirring the graphite, silicon monoxide, and carbon precursor are not particularly limited, and optimal conditions are selected as appropriate according to the materials used.
  • the stirring time is preferably approximately 1 to 2 hours because the graphite, silicon monoxide, and carbon precursor can be more uniformly dispersed, and as a result, the cycle characteristics of a lithium secondary battery that uses the obtained composite active material for lithium secondary batteries are better.
  • ultrasonic waves may be applied as necessary while stirring.
  • the stirring time should be approximately 10 minutes.
  • the method for removing the solvent is not particularly limited, and a method using a known apparatus (for example, an evaporator) or the like may be employed.
  • the mixing ratio of graphite and silicon monoxide is not particularly limited, but is preferably from 10 to 230 parts by mass and more preferably from 20 to 200 parts by mass of silicon monoxide relative to 100 parts by mass of graphite because the effects of the present invention are better.
  • the mixing ratio of graphite and carbon precursor is not particularly limited, but is preferably from 1 to 50 parts by mass and more preferably from 5 to 20 parts by mass of carbon precursor relative to 100 parts by mass of graphite because the effects of the present invention are better.
  • the mixing ratio of silicon monoxide and carbon precursor is not particularly limited, but is preferably from 0.1 to 100 parts by mass and more preferably from 1 to 50 parts by mass of carbon precursor relative to 100 parts by mass of silicon monoxide because the effects of the present invention are better.
  • the used amount thereof is not particularly limited, but since the effects of the present invention are better as a result of a higher degree of dispersion, it is preferably from 3000 to 15,000 parts by mass and more preferably from 5000 to 7000 parts by mass of solvent relative to 100 parts by mass of graphite.
  • a pressing step of pressing the obtained mixture may be included as necessary.
  • the distance between graphite particles is smaller and the conglobation treatment proceeds more efficiently.
  • the method of pressing is not particularly limited, and a known method may be employed.
  • the conglobation step is a step in which conglobation treatment is performed on the mixture containing graphite, silicon monoxide, and a carbon precursor obtained in the above mixing step, to produce a spherical mixture.
  • the graphite sheets are folded and conglobated so as to incorporate the silicon monoxide and carbon precursor inside them. At that time, a structure is obtained in which the edge parts of the graphite are folded to the inside and substantially no silicon monoxide is exposed on the surface of the composite active material for lithium secondary batteries.
  • the long axis direction - that is, the AB plane - of the graphite aligns in the direction of the airflow and collides with pins or collision plates placed perpendicular to the airflow, or the particles of the graphite-precursor material mixture collide with each other, and the AB plane of the graphite is compressed and deformed and consequently undergoes conglobation in a form where it sandwiches the precursor material.
  • the long axis of expanded graphite is the C axis direction of the graphite
  • the C axis of the graphite aligns in the direction of the airflow and collides with the pins or collision plates, or the particles collide with each other.
  • the C axis of the graphite is compressed and the graphite is changed to a state close to its pre-expansion form. This means that the precursor material attached to the AB plane of the graphite is crushed by the graphite and completely sandwiched by the graphite layers.
  • the graphite compressed in the C axis direction changes to a structure in which the AB plane serves as the long axis, and eventually the AB plane of the graphite changes to a folded spherical body.
  • the laminated graphene sheet layers that constitute expanded graphite or flake graphite are thin, the AB plane is easily deformed by a smaller compressive force in the direction of the AB plane.
  • the method of conglobation treatment is not particularly limited as long as a crusher that can mainly apply impact stress is used.
  • the crusher include a high-speed rotary impact crusher, and more specifically, a sample mill, hammer mill, pin mill, or the like may be used. Above all, a pin mill is preferred because mixing of the graphite and the precursor material is more uniform and the effects of the present invention are better.
  • the high-speed rotary impact crusher may be one that causes a sample to collide with a rotor which rotates at high speed and crushes it into fine particles using the impact force thereof.
  • Examples include a hammer type of hammer mill in which a stationary-style or swinging-style impactor is mounted on a rotor, a rotating disk type of pin mill in which pins or collision heads are mounted on rotating disks, an axial flow type which crushes the sample while it is fed in the direction of the shaft, and an annular type which makes particles fine using narrow ring-shaped parts. More specific examples include a hammer mill, pin mill, screen mill, turbo mill, centrifugal classifier-type mill, and the like.
  • this step is performed using a high-speed rotary impact crusher, conglobation is performed at a rotation speed of normally not less than 100 rpm, preferably not less than 1500 rpm, and normally not greater than 20,000 rpm. Therefore, the collision speed is preferably approximately from 20 m/sec to 100 m/sec.
  • conglobation treatment is performed with low impact force, unlike crushing, circulating treatment is preferably performed in this step.
  • the treatment time varies depending on the type of crusher used and the quantity loaded, but normally it is 2 minutes or less, and treatment is completed in approximately 10 seconds as long as it is an apparatus in which appropriate pins or collision plates are arranged.
  • conglobation treatment is preferably performed in air.
  • this treatment is performed under nitrogen flow, there is danger of ignition when opened to the atmosphere.
  • the size of the spherical mixture obtained by the above conglobation treatment is not particularly limited, but the particle size of the spherical mixture (D50: 50% volume particle diameter) is preferably from 2 to 40 ⁇ m, more preferably from 5 to 35 ⁇ m, and even more preferably from 5 to 30 ⁇ m, because the effects of the present invention are better.
  • D50 corresponds to the 50% cumulative particle diameter from the fine side of the cumulative particle size distribution measured by the laser diffraction/scattering measurement method.
  • the spherical mixture is added to a liquid and mixed vigorously while using ultrasonic waves or the like, and the produced dispersion is introduced into the apparatus as a sample and measured.
  • the liquid water, alcohol, or a low-volatility organic solvent is preferred due to ease of handling. It is preferred that the obtained particle size distribution be a normal distribution at that time.
  • the heating step is a step of heat-treating the spherical mixture obtained as described above and producing a substantially spherical composite active material for lithium secondary batteries (composite active material).
  • the composite active material contains a graphite component derived from the aforementioned graphite and a composite containing silicon and silicon dioxide (silicon-containing composite), and the composite is encapsulated in the graphite component as will be described later.
  • the composite contains silicon and silicon dioxide
  • the state of dispersion of the two is not particularly limited, and may be, for example, a sea-and-island state of dispersion. Above all, it is preferably a composite in which silicon is dispersed in silicon dioxide because the effects of the present invention are better. Furthermore, some of the precursor silicon monoxide sometimes may remain in the composite.
  • the heating temperature is preferably not less than 700°C and more preferably not less than 800°C because the effects of the present invention are better.
  • the upper limit is not particularly limited but is preferably not greater than 2000°C, more preferably not greater than 1500°C, and even more preferably not greater than 1000°C.
  • the heating time is preferably not less than 0.5 hours and more preferably not less than 1 hour.
  • the upper limit is not particularly limited but is often not greater than 5 hours because the effects of the present invention become saturated and because fine crystals of silicon are of a preferred size.
  • the atmosphere in which heat treatment is performed is preferably an inert atmosphere because it prevents oxidation of silicon and carbon.
  • FIG. 1 is a schematic view of an embodiment of a composite active material.
  • a composite active material 10 is substantially spherical, and as the structure thereof, a composite 14 is encapsulated in a graphite component 12, and in the composite 14, silicon 18 is dispersed in silicon dioxide 16. Note that a composite in which silicon is dispersed in silicon dioxide is described above, but it is not limited to this mode.
  • the obtained composite active material will be described in detail below.
  • the shape of the composite active material is substantially spherical because of the treatment described above.
  • substantially spherical means that the composite active material has a structure having roundness and is a shape that does not have sharp edges (peaks and jutting parts) as are generally seen in fractured particles.
  • substantially spherical indicates a shape of composite active material in which the aspect ratio, which is the ratio of the long diameter to the short diameter (long diameter/short diameter) is approximately in the range of 1 to 3 (more preferably 1 to 2 because the effects of the present invention are better).
  • the aspect ratio signifies the arithmetic mean of the values of long diameter/short diameter of at least 100 particles.
  • the short diameter in the above description is the distance between the two parallel lines that result in the shortest distance among the combinations of two parallel lines touching the outside of and sandwiching a particle observed by scanning electron microscope.
  • the long diameter is the distance between the two parallel lines that result in the longest distance among the combinations of two parallel lines touching the outside of a particle and orthogonal to the parallel lines that determine the short diameter.
  • the rectangle formed by these four lines has a size that the particle just fits into.
  • the area ratio of the graphite component exposed on the composite active material surface observed by scanning electron microscope (SEM) at acceleration voltage of not greater than 10 kV is not less than 95%. Above all, not less than 98% is more preferred, and not less than 99% is even more preferred.
  • the upper limit is not particularly limited, and may be 100%. As long as the area ratio is within the above range, the amount of composite exposed on the surface of the composite active material is small, and as a result, volume expansion of an electrode material that contains the composite active material is suppressed and a lithium secondary battery that contains the composite active material exhibits excellent cycle characteristics.
  • the composite readily sloughs off and cycle characteristics are inferior, or volume expansion of an electrode material containing the composite is large.
  • At least 100 particles of composite active material are observed by scanning electron microscope (SEM) at acceleration voltage of not greater than 10 kV (preferably at a magnification of not less than 2000X), and the area ratio of the graphite component relative to the surface of each composite active material particle is measured, and the arithmetic mean thereof is taken as the area ratio.
  • SEM scanning electron microscope
  • the area ratio of the composite exposed on the composite active material surface observed by scanning electron microscope (SEM) at acceleration voltage of not greater than 10 kV is preferably not greater than 5%. Above all, not greater than 2% is more preferred, and not greater than 1% is even more preferred.
  • the lower limit is not particularly limited, and may be 0%. As long as the area ratio is within the above range, the amount of composite exposed on the surface of the composite active material is small, and as a result, volume expansion on an electrode material that contains the composite active material is suppressed and a lithium secondary battery that contains the composite active material exhibits excellent cycle characteristics.
  • At least 100 particles of composite active material are observed by scanning electron microscope (SEM) at acceleration voltage of not greater than 10 kV (preferably at magnification of not less than 2000X), and the area ratio of the composite relative to the surface of each composite active material particle is measured, and the arithmetic mean thereof is taken as the area ratio.
  • SEM scanning electron microscope
  • a feature of the composite active material for lithium secondary batteries is that when observed by scanning electron microscope (SEM) at acceleration voltage of not greater than 10 kV, the composite that has penetrated through the thin graphite layer and has been encapsulated in a state sandwiched in graphite layers can be observed directly.
  • SEM scanning electron microscope
  • a preferred mode of the composite active material is a mode in which substantially no edge parts of the graphite are exposed on the surface thereof. Due to no edge parts being exposed on the surface, degradation of the electrolyte and destruction of the graphite, which readily occur during the charge-discharge cycle, are suppressed, resulting in improved cycle characteristics.
  • the graphite component in the composite active material is the graphite-derived component described above. Note that because conglobation treatment is performed at the time of formation of the composite active material, the above-described graphite may also take on a folded structure in the composite active material.
  • the content of the composite in the composite active material may be adjusted as appropriate according to the content of silicon monoxide in the mixing step described above.
  • the content of the composite is preferably not less than 10 mass%, more preferably 20 mass%, and particularly preferably not less than 30 mass% relative to the total amount of composite active material because the effects of the present invention are better.
  • the upper limit is preferably not greater than 80 mass% and more preferably not greater than 70 mass%.
  • the area ratio of the graphite component exposed on the composite active material surface is within the above range even when the content of the composite is within the above range.
  • the shape of the composite in the composite active material is not particularly limited, but is normally substantially spherical in many cases.
  • the composite active material may also contain a large number of composite particles, as illustrated in FIG. 1 .
  • the average particle size of the composite in the composite active material is not particularly limited but is preferably not greater than 1 ⁇ m, more preferably not greater than 0.5 ⁇ m, and even more preferably not greater than 0.3 ⁇ m because the effects of the present invention are better.
  • the lower limit is not particularly limited and is preferably low (not less than 50 nm in many cases).
  • the method for measuring the average particle size a cross-section of the composite active material is observed by electron microscope and the diameter of at least 10 composite particles is measured, and the arithmetic mean thereof is taken as the average particle size. Note that when the composite does not have a perfectly circular shape, the circular equivalent diameter is used.
  • the "circular equivalent diameter" is the diameter of a circle having the same projected area as the projected area of the composite when it is assumed that the shape of the observed composite is that circle.
  • the composite contains silicon and silicon dioxide, and the silicon is preferably encapsulated in the silicon dioxide.
  • the composite may also contain a large number of silicon particles, as illustrated in FIG. 1 .
  • the average particle size of silicon in the composite is not particularly limited but is preferably from 1 to 100 nm and more preferably from 1 to 20 nm because the effects of the present invention are better.
  • TEM electron microscope
  • the content of silicon in the composite is not particularly limited but is preferably from 20 to 200 mass% and more preferably from 40 to 150 mass% relative to the total mass of silicon dioxide in the composite because the effects of the present invention are better.
  • silicon dioxide (SiO 2 ) in the composite may be removed as necessary using HF or the like.
  • the amount of silicon dioxide on the silicon (Si) surface can be adjusted by varying the amount of etching. From the perspective of protecting the surface, it is preferable to leave a certain amount of silicon dioxide.
  • the relative mass of Si which is the active material can be increased and capacity can be increased.
  • the voids left after silicon dioxide has been removed can be decreased using an apparatus that isotropically applies force, such as a mill used in conglobation.
  • the content of silicon may be increased by eluting SiO 2 with HF, and in that case, the content of silicon may be adjusted to 100 to 9900 mass% relative to the total mass of silicon dioxide in the composite.
  • the content of silicon may be measured by ICP emission spectroscopy.
  • the composite active material normally contains a carbide derived from a carbon precursor (carbon material; for example, hard carbon, soft carbon, or the like).
  • the content of the carbide in the composite active material may be adjusted as appropriate according to the content of carbon precursor in the mixing step described above.
  • the carbide content is preferably not less than 1 mass%, more preferably not less than 2 mass%, and particularly preferably not less than 5 mass% relative to the total amount of composite active material because the effects of the present invention are better.
  • the upper limit is preferably not greater than 30 mass% and more preferably not greater than 20 mass%.
  • the particle diameter (D50: 50% volume diameter) of the composite active material is not particularly limited but is preferably from 2 to 40 ⁇ m, more preferably from 5 to 35 ⁇ m, and even more preferably from 5 to 30 ⁇ m because the effects of the present invention are better.
  • the particle diameter (D90: 90% volume diameter) is not particularly limited but is preferably from 10 to 60 ⁇ m and more preferably from 20 to 45 ⁇ m because the effects of the present invention are better.
  • the particle diameter (D10: 10% volume diameter) is not particularly limited but is preferably from 1 to 20 ⁇ m and more preferably from 2 to 10 ⁇ m because the effects of the present invention are better.
  • D10, D50, and D90 correspond to the 10%, 50%, and 90% cumulative particle diameter from the fine side of the cumulative particle size distribution measured by the laser diffraction/scattering measurement method.
  • the composite active material when measurement is performed, the composite active material is added to a liquid and mixed vigorously while using ultrasonic waves or the like, and the produced dispersion is introduced into the apparatus as a sample and measured.
  • the liquid water, alcohol, or a low-volatility organic solvent is preferred due to ease of handling. It is preferred that the obtained particle size distribution be a normal distribution at that time.
  • the bulk density of the composite active material is not particularly limited but is preferably not less than 0.5 g/cm 3 and more preferably not less than 0.7 g/cm 3 because the capacity per volume of obtained composite active material is larger.
  • the upper limit is not particularly limited.
  • the method for measuring bulk density is the same as the method for measuring the bulk density of graphite described above except that a 25-mL graduated cylinder is used.
  • the tap density of the composite active material is not particularly limited but is preferably not less than 0.8 g/cm 3 and more preferably not less than 1.0 g/cm 3 because the capacity per volume of obtained composite active material is larger.
  • the upper limit is not particularly limited, but not greater than 1.6 g/cm 3 is preferred.
  • a sample is inserted in a 25-mL graduated cylinder, it is tapped, and tap density is determined by dividing the sample weight by the sample volume at the point when there is no longer any change in volume.
  • the specific surface area (BET specific surface area) of the composite active material is not particularly limited but is preferably not less than 5 m 2 /g and more preferably not less than 8 m 2 /g because the cycle characteristics of a lithium secondary battery that uses the obtained composite active material are better.
  • the upper limit is not particularly limited, but not greater than 100 m 2 /g is preferred.
  • the sample is measured by the nitrogen adsorption single-point method after vacuum-drying for 30 minutes at 300°C.
  • the surface of the composite active material may be covered with carbon as necessary. By implementing such treatment, the surface area of the composite active material may be adjusted and electrochemical stability may be increased.
  • the method for covering with carbon is not particularly limited but may be CVD, for example. More specifically, it is preferable to perform CVD treatment at 750 to 1100°C under the flow of a gas such as toluene.
  • the composite active material described above is useful as an active material used in battery materials (electrode materials) used in lithium secondary batteries.
  • battery materials that use the above composite active material are that capacity is close to the theoretical value of the battery material and that expansion is suppressed. Furthermore, a battery that uses this battery material exhibits excellent cycle characteristics. Additionally, ultra-fast charging and discharging characteristics are excellent because the diffusion length of Li ions is small as a result of silicon having been made into fine particles.
  • composite active material is preferably used in the anode.
  • a mode using the composite active material in an anode will be described in detail below.
  • the method for producing an anode for lithium secondary batteries using the composite active material is not particularly limited, and a known method may be used.
  • an anode for lithium secondary batteries may be produced by mixing the composite active material and a binder, making it into a paste using compression molding or a solvent, and applying it to copper foil. More specifically, 92 g of composite active material, 62 g of 13% PVDF/NMP solution, 0.5 g of conductive carbon black, and 29 g of NMP are mixed, and a good slurry is obtained using a typical dual arm mixer.
  • a material having a three-dimensional structure may also be used as a current collector because the cycle characteristics of the battery are better.
  • materials of a current collector having a three-dimensional structure include carbon fibers, sponge-like carbon (carbon applied to sponge-like resin), metals, and the like.
  • Examples of a current collector (porous current collector) having a three-dimensional structure include, as porous bodies of metal or carbon current collectors, plain weave metal mesh, expanded metal, lath mesh, metal foam, metal fabric, metal non-woven fabric, carbon fiber fabric, carbon fiber non-woven fabric, and the like.
  • the binder used may be a known material, examples of which include fluorine resins such as polyvinylidene fluoride and polytetrafluoroethylene, SBR, polyethylene, polyvinyl alcohol, carboxymethylcellulose, glue, and the like.
  • fluorine resins such as polyvinylidene fluoride and polytetrafluoroethylene, SBR, polyethylene, polyvinyl alcohol, carboxymethylcellulose, glue, and the like.
  • solvent examples include water, isopropyl alcohol, N-methylpyrrolidone, dimethylformamide, and the like.
  • stirring and mixing may be performed using a known stirrer, blender, mixer, kneader, or the like according to need, as described above.
  • conductive carbon black, carbon nanotubes, or a mixture thereof as a conductive material.
  • the shape of the composite active material obtained by the above steps is often relatively particulate (especially substantially spherical), and contact between particles tends to be point contact.
  • methods in which carbon black, carbon nanotubes, or a mixture thereof is blended in the slurry may be employed.
  • Carbon black, carbon nanotubes, or a mixture thereof can prevent the disconnection of contact points (increased resistance) which accompanies cycling because they aggregate in a concentrated manner in the capillary portions formed by contact with the composite active material when the slurry solvent is dried.
  • the blended amount of carbon black, carbon nanotubes, or a mixture thereof is not particularly limited but is preferably from 0.2 to 4 part by mass and more preferably from 0.5 to 2 parts by mass relative to 100 parts by mass of composite active material.
  • Examples of carbon nanotubes include single-wall carbon nanotubes and multi-wall carbon nanotubes.
  • Cathodes that use known cathode materials may be used as the cathode used in a lithium secondary battery having an anode obtained using the above composite active material.
  • cathode active material examples include metal oxides such as chromium oxide, titanium oxide, cobalt oxide, and vanadium pentoxide; lithium metal oxides such as LiCoO 2 , LiNiO 2 , LiNi 1-y Co y O 2 , LiNi 1-x-y Co x Al y O 2 , LiMnO 2 , LiMn 2 O 4 , and LiFeO 2 ; transition metal chalcogen compounds such as titanium sulfide and molybdenum sulfide; and conductive conjugated polymer materials such as polyacetylene, polyparaphenylene, and polypyrrole.
  • metal oxides such as chromium oxide, titanium oxide, cobalt oxide, and vanadium pentoxide
  • lithium metal oxides such as LiCoO 2 , LiNiO 2 , LiNi 1-y Co y O 2 , LiNi 1-x-y Co x Al y O 2 , LiMnO 2 , LiMn 2 O 4
  • electrolytes may be used as the electrolyte used in a lithium secondary battery having an anode obtained using the above composite active material.
  • electrolyte salts that may be contained in the electrolyte include lithium salts such as LiPF 6 , LiBF 4 , LiAsF 6 , LiClO 4 , LiB(C 6 H 5 ), LiCl, LiBr, LiCF 3 SO 3 , LiCH 3 SO 3 , LiN(CF 3 SO 2 ) 2 , LiC(CF 3 SO 2 ) 3 , LiN(CF 3 CH 2 OSO 2 ) 2 , LiN(CF 3 CF 3 OSO 2 ) 2 , LiN(HCF 2 CF 2 CH 2 OSO 2 ) 2 , LiN ⁇ (CF 3 ) 2 CHOSO 2 ⁇ 2 , LiB ⁇ (C 6 H 3 (CF 3 ) 2 ⁇ 4 , LiN(SO 2 CF 3 ) 2 , LiC(SO 2 CF 3 ) 3 , LiAlCl 4 , and LiSiF 6 .
  • LiPF 6 and LiBF 4 are particularly preferred from the perspective of oxidation stability.
  • the electrolyte salt concentration in the electrolyte solution is preferably from 0.1 to 5 mol/L and more preferably from 0.5 to 3 mol/L.
  • solvent used in the electrolyte examples include carbonates such as ethylene carbonate, propylene carbonate, dimethyl carbonate, and diethyl carbonate; ethers such as 1,1- or 1,2-dimethoxyethane, 1,2-diethoxyethane, tetrahydrofuran, 2-methyltetrahydrofuran, ⁇ -butyrolactone, 1,3-dioxofuran, 4-methyl-1,3-dioxolane, anisole, and diethyl ether; thioethers such as sulfolane and methylsulfolane; nitriles such as acetonitrile, chloronitrile, and propionitrile; and organic aprotic solvents such as trimethyl borate, tetramethyl silicate, nitromethane, dimethylformamide, N-methylpyrrolidone, ethyl acetate, trimethyl orthoformate, nitrobenzene, benzoyl chloride, benzoyl bromid
  • Additives such as fluoroethylene carbonate and the like may also be added to the electrolyte. These additives form a stable protective film on the silicon surface and are known to improve cycle characteristics.
  • a polymer electrolyte such as polymer solid electrolyte or polymer gel electrolyte may also be used.
  • ether-based polymer compounds such as polyethylene oxide or cross-linked compounds thereof; methacrylate-based polymer compounds such as polymethacrylate; acrylate-based polymer compounds such as polyacrylate; and fluorine-based polymer compounds such as polyvinylidene fluoride (PVDF) and vinylidene fluoride-hexafluoropropylene copolymer may be used. These may also be used as mixtures. From the perspective of oxidation-reduction stability, fluorine-based polymer compounds such as polyvinylidene fluoride (PVDF) and vinylidene fluoride-hexafluoropropylene copolymer are particularly preferred.
  • Known materials may be used as the separator used in a lithium secondary battery having an anode obtained using the above composite active material.
  • Examples include fabric, non-woven fabric, synthetic microporous resin film, and the like.
  • Synthetic microporous resin films are advantageous, among which polyolefin-based microporous films are advantageous from the perspectives of film thickness, film strength, film resistance, and the like.
  • examples include polyethylene and polypropylene microporous films, microporous films that are composites thereof, and the like.
  • a lithium secondary battery may have the form of a cylinder, a rectangle, or a button produced by customary methods using the above-described anode, cathode, separator, electrolyte, and other constituent elements of a battery (for example, the current collector, gasket, seal sheet, case, and the like).
  • the lithium secondary battery of the present invention may be used in various portable electronic devices, especially notebook PCs, notebook word processors, palmtop (pocket) PCs, cellular telephones, portable fax machines, portable printers, headphone stereos, video cameras, portable televisions, portable CD players, portable minidisc players, electric shavers, electronic organizers, transceivers, power tools, radios, tape recorders, digital cameras, portable copiers, portable game devices, and the like. Furthermore, it may also be used as a secondary battery for electric automobiles, hybrid automobiles, vending machines, electric carts, capacitor systems for load leveling, household capacitors, distributed power storage device systems (built into deferred operation products), emergency power supply systems, and the like.
  • Scaly natural graphite having an average particle size of 1 mm was soaked for 1 hour in a mixed acid containing 9 parts by weight of sulfuric acid and 1 part by weight of nitric acid, and then the mixed acid was removed with a no. 3 glass filter, to obtain acid-treated graphite.
  • the acid-treated graphite was then washed with water and dried. Then, 5 g of the dried acid-treated graphite was stirred in 100 g of distilled water, and when the pH was measured after 1 hour it was 6.7.
  • the dried acid-treated graphite was put in a vertical electric furnace in a nitrogen atmosphere set to 850°C, to obtain expanded graphite.
  • the bulk density of the acid-treated graphite was 0.78 g/cm 3 .
  • the specific surface area of the expanded graphite was 83 m 2 /g, the bulk specific gravity was 0.011 g/cm 3 , and the average thickness of the layer of laminated graphene sheets was 16 nm.
  • the above expanded graphite (12 parts by mass) was added to ethanol in which SiO was dispersed, to prepare a uniformly mixed slurry containing expanded graphite, SiO fine powder, and phenol resin.
  • the ethanol was recovered from the slurry using an evaporator, and a powder mixture was obtained.
  • the powder mixture obtained as described above was granulation-molded into a spherical shape using a New Power Mill PM-2005M-1380W (Osaka Chemical Co., Ltd.) (rotational speed: 20,000 rpm, treatment time: 90 seconds, performed 10 times).
  • the area ratio of graphite exposed on the surface of the composite active material for lithium secondary batteries observed by SEM was 98%, and the area ratio of exposed composite was 2%.
  • PVDF polyvinylidene fluoride
  • a cycle test was conducted using the above full cell, and then the cell was disassembled and the electrodes removed, and the change in thickness of the electrodes ⁇ (electrode thickness after test - electrode thickness before test)/(electrode thickness before test) ⁇ 100 ⁇ was measured. Furthermore, a cycle experiment was conducted using a charging and discharging rate of C/3 (0.18 mA) with a cutoff voltage on the charging side of 4.2 V and a cutoff voltage on the discharging side of 3.0 V.
  • the shape of the electrode before the cycle test was a disc 14 mm in diameter of thickness 55 ⁇ m.
  • the thickness was an average value, determined by measuring the thickness at the center of the disc and any other three points and taking the arithmetic mean thereof.
  • the thickness of the electrodes after the cycle test was similarly determined by measuring the thickness at the center of the disc and any other three points and taking the arithmetic mean thereof.
  • the capacity retention rate in the 11 th cycle was measured based on the average discharge capacity (mAh) in the second cycle.
  • Substantially spherical composite active material for lithium secondary batteries comprising 70 mass% of graphite and 30 mass% of metallic Si was obtained according to Example 1 of Patent Document 1 (Japanese Patent No. 5227483B ).
  • Example 1 Average discharge capacity (2 nd cycle) Average discharge capacity (11 th cycle) Capacity retention rate (%) Coulombic efficiency th (10 th cycle) Electrode expansion rate (10 th cycle) Example 1 1.79 1.77 98.8 99.30% 13% Comparative Example 1 2.34 2.04 87.1 98.50% 35%
  • the full cell that used the composite active material for lithium secondary batteries of the present invention exhibited excellent capacity retention rate and Coulombic efficiency, and it was ascertained to have excellent cycle characteristics. It was also ascertained that expansion of the electrodes containing this composite active material was suppressed.
  • Comparative Example 1 which is a mode of Patent Document 1, the cycle characteristics of the full cell were poor and electrode expansion was larger compared to the example above.
  • the composite active material according to the present invention may be used as an electrode material of a lithium secondary battery.

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Claims (8)

  1. Matière composite active pour batterie rechargeable au lithium comprenant :
    un composite contenant du silicium et du dioxyde de silicium ; et
    un composant graphite ;
    le rapport en surface du composant graphite exposé sur une surface observée au microscope électronique à balayage à une tension d'accélération inférieure ou égale à 10 kV n'étant pas inférieur à 95 %.
  2. Matière composite active pour batterie rechargeable au lithium selon la revendication 1, dans laquelle une taille de particule moyenne du silicium est de 1 à 100 nm.
  3. Matière composite active pour batterie rechargeable au lithium selon la revendication 1 ou 2, dans laquelle une taille de particule moyenne du composite est de 50 à 1000 nm.
  4. Procédé de production de la matière composite active pour batterie rechargeable au lithium décrite à la revendication 1, comprenant :
    une étape de mélange comprenant le mélange d'un graphite ayant une surface spécifique égale ou supérieure à 30 m2/g, du monoxyde de silicium, et d'un précurseur de carbone pour obtenir un mélange ;
    une étape de conglobation comprenant l'application d'un traitement de conglobation au mélange et l'obtention d'un mélange sphérique ; et
    une étape de chauffage comprenant le traitement thermique du mélange sphérique et la production d'une matière composite active pour batterie rechargeable au lithium sensiblement sphérique.
  5. Procédé de production d'une matière composite active pour batterie rechargeable au lithium selon la revendication 4, dans lequel une taille de particule moyenne du monoxyde de silicium n'est pas supérieure à 1 µm.
  6. Procédé de production d'une matière composite active pour batterie rechargeable au lithium selon la revendication 4 ou 5, dans lequel
    le précurseur de carbone est au moins d'un type choisi dans le groupe constitué par les composés polymères, une poix à base de charbon, une poix à base de pétrole, une poix à l'état de mésophase, le coke, une huile de bas poids moléculaire, et des dérivés de ceux-ci.
  7. Procédé de production d'une matière composite active pour batterie rechargeable au lithium selon l'une quelconque des revendications 4 à 6, dans lequel le graphite est un graphite expansé.
  8. Batterie rechargeable au lithium comprenant la matière composite active pour batterie rechargeable au lithium décrite dans l'une quelconque des revendications 1 à 3.
EP14836628.9A 2013-08-14 2014-08-12 Matière active composite pour des batteries rechargeables au lithium et procédé de fabrication de cette dernière Active EP3035418B1 (fr)

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Families Citing this family (14)

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Publication number Priority date Publication date Assignee Title
EP3133690A1 (fr) * 2015-07-20 2017-02-22 Commissariat A L'energie Atomique Et Aux Energies Alternatives Matériau particulaire composite silicium-carbone
JP6733248B2 (ja) * 2016-03-22 2020-07-29 東ソー株式会社 リチウム二次電池用複合活物質の製造方法
EP3497055B1 (fr) * 2016-08-11 2022-03-16 Wacker Chemie AG Préparation de particules precomposites de si/c
SG11202000089TA (en) * 2016-10-11 2020-02-27 Grst Int Ltd Cathode slurry for lithium ion battery
WO2018098506A1 (fr) * 2016-11-28 2018-05-31 Sila Nanotechnologies Inc. Électrodes de batterie à capacité élevée dotées de liants, de construction et de performances améliorés
WO2018179111A1 (fr) * 2017-03-28 2018-10-04 日立化成株式会社 Matériau actif d'électrode négative pour batterie secondaire lithium-ion, électrode négative pour batterie secondaire lithium-ion, et batterie secondaire lithium-ion
US10714745B2 (en) 2017-07-28 2020-07-14 Uchicago Argonne, Llc High energy, long cycle life electrode for lithium-ion batteries
CN107623113A (zh) * 2017-09-08 2018-01-23 赣州市瑞富特科技有限公司 一种多孔长循环硅碳负极材料制备方法
KR102244953B1 (ko) * 2017-11-09 2021-04-27 주식회사 엘지화학 음극 활물질, 상기 음극 활물질을 포함하는 음극, 및 상기 음극을 포함하는 이차 전지
JP6978947B2 (ja) * 2018-01-12 2021-12-08 株式会社クレハ 電池用負極材料及びその製造方法、二次電池用負極、並びに二次電池
KR20200110754A (ko) * 2018-01-31 2020-09-25 히타치가세이가부시끼가이샤 리튬 이온 이차 전지용 음극 활물질, 리튬 이온 이차 전지용 음극 및 리튬 이온 이차 전지
CN111656584A (zh) * 2018-01-31 2020-09-11 日立化成株式会社 锂离子二次电池用负极活性物质、锂离子二次电池用负极和锂离子二次电池
CN114744167B (zh) * 2022-03-10 2024-02-27 合盛科技(宁波)有限公司 一种氧化亚硅/膨胀石墨/碳复合材料及其制备方法
CN115911303A (zh) * 2022-10-25 2023-04-04 广东容钠新能源科技有限公司 一种高倍率硅基硬炭材料的制备方法及应用

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20060068287A1 (en) * 2004-09-24 2006-03-30 Kabushiki Kaisha Toshiba Negative electrode active material for nonaqueous electrolyte secondary battery and nonaqueous electrolyte secondary battery

Family Cites Families (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI278429B (en) 2002-05-17 2007-04-11 Shinetsu Chemical Co Conductive silicon composite, preparation thereof, and negative electrode material for non-aqueous electrolyte secondary cell
JP2004119176A (ja) * 2002-09-26 2004-04-15 Toshiba Corp 非水電解質二次電池用負極活物質及び非水電解質二次電池
JP3995050B2 (ja) 2003-09-26 2007-10-24 Ｊｆｅケミカル株式会社 リチウムイオン二次電池負極材料用複合粒子およびその製造方法、リチウムイオン二次電池用負極材料および負極、ならびにリチウムイオン二次電池
KR100578870B1 (ko) 2004-03-08 2006-05-11 삼성에스디아이 주식회사 리튬 이차 전지용 음극 활물질, 그의 제조 방법 및 그를포함하는 리튬 이차 전지
JP4533822B2 (ja) * 2005-08-24 2010-09-01 株式会社東芝 非水電解質電池および負極活物質
JP2008027897A (ja) 2006-06-20 2008-02-07 Osaka Gas Chem Kk リチウムイオン二次電池用負極活物質
JP5143437B2 (ja) * 2007-01-30 2013-02-13 日本カーボン株式会社 リチウムイオン二次電池用負極活物質の製造方法、負極活物質及び負極
KR101375328B1 (ko) 2007-07-27 2014-03-19 삼성에스디아이 주식회사 Ｓｉ／Ｃ 복합물, 이를 포함하는 음극활물질 및 리튬전지
JP5272492B2 (ja) * 2008-04-21 2013-08-28 信越化学工業株式会社 非水電解質二次電池用負極材及びその製造方法、ならびに非水電解質二次電池用負極及び非水電解質二次電池
US9093693B2 (en) * 2009-01-13 2015-07-28 Samsung Electronics Co., Ltd. Process for producing nano graphene reinforced composite particles for lithium battery electrodes
US8778538B2 (en) 2009-11-06 2014-07-15 Northwestern University Electrode material comprising graphene-composite materials in a graphite network
US9558860B2 (en) * 2010-09-10 2017-01-31 Samsung Electronics Co., Ltd. Graphene-enhanced anode particulates for lithium ion batteries
JP5691468B2 (ja) 2010-12-10 2015-04-01 日立化成株式会社 リチウムイオン二次電池用負極材及びその製造方法、リチウムイオン二次電池用負極、並びにリチウムイオン二次電池
CN103262314B (zh) * 2010-12-10 2015-07-01 日立化成株式会社 锂离子二次电池用负极材料及其制造方法、锂离子二次电池用负极和锂离子二次电池
JP2013073920A (ja) * 2011-09-29 2013-04-22 Sumitomo Bakelite Co Ltd 組成物、リチウムイオン二次電池負極材用炭素複合材、リチウムイオン二次電池用負極合剤、リチウムイオン二次電池用負極、及びリチウムイオン二次電池
JP5639017B2 (ja) 2011-07-29 2014-12-10 住友ベークライト株式会社 リチウムイオン二次電池用負極活物質、リチウムイオン二次電池用負極合剤、リチウムイオン二次電池用負極、及びリチウムイオン二次電池
KR20140026633A (ko) 2011-07-29 2014-03-05 스미토모 베이클리트 컴퍼니 리미티드 리튬 이온 2차 전지용 탄소재의 제조 방법, 리튬 이온 2차 전지용 탄소재, 리튬 이온 2차 전지용 부극 활물질, 조성물, 리튬 이온 2차 전지 부극재용 탄소 복합재, 리튬 이온 2차 전지용 부극 합제, 리튬 이온 2차 전지용 부극 및 리튬 이온 2차 전지
CN103891015B (zh) * 2011-08-22 2017-05-24 可知直芳 锂二次电池用复合活性物质及其制造方法
JP5636351B2 (ja) 2011-09-27 2014-12-03 株式会社東芝 非水電解質二次電池用負極活物質、非水電解質二次電池、電池パック及び非水電解質二次電池用負極活物質の製造方法
JP2013219018A (ja) 2012-03-11 2013-10-24 Ｃｏｎｎｅｘｘ Ｓｙｓｔｅｍｓ株式会社 リチウム二次電池用複合活物質およびその製造方法
EP2960971B1 (fr) 2013-02-21 2020-04-22 Connexx Systems Corporation Substance active composite pour batterie secondaire au lithium ainsi que procédé de production de celle-ci

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20060068287A1 (en) * 2004-09-24 2006-03-30 Kabushiki Kaisha Toshiba Negative electrode active material for nonaqueous electrolyte secondary battery and nonaqueous electrolyte secondary battery

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CN105453310A (zh) 2016-03-30
US20160197345A1 (en) 2016-07-07
EP3035418A1 (fr) 2016-06-22
US10749178B2 (en) 2020-08-18
JP2015037057A (ja) 2015-02-23
JP6508870B2 (ja) 2019-05-08
WO2015022964A1 (fr) 2015-02-19

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